US4661612A
Expired / Lapsed
US
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Method for purifying silicone oil
Assignee: Telefunken Systemtechnik AG
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Filing: 1985-11-13
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Granted: 1987-04-28
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Expires: 2005-11-13
Abstract
Abstract A method for purifying silicone oil used particularly as a cooling and/or insulation agent in electrical high voltage devices. The silicone oil is purified by the addition of drying agents, e.g. molecular sieves, and adsorption agents, e.g. activated carbon, and by mechanically moving the mixture. After subsequent sedimentation, filtration and degasification, purified silicone oil is obtained which can again be used as a coolant and/or insulating agent.
Inventors
- 👤 Ulf George
- 👤 Erwin Rochau
- 👤 Hans Merk
- 👤 Joachim Behnke
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 10:52
CPC Classifications
C; C08; C08G; C08G77/00; C08G77/04; C08G77/32; C08G77/34; H; H01; H01B; H01B3/00; H01B3/18; H01B3/30; H01B3/46; H01B3/465
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
130 words
Process for purifying silicone oil to remove impurities contained therein, comprising: adding a drying agent and an adsorption agent to the silicone oil, said adsorption agent selected from the group consisting of activated carbon and activated fuller's earth and said drying agent selected from the group consisting of molecular sieves, silica gel and activated aluminum oxide; causing the drying agent and the adsorption agent to act on the silicone oil during a reaction period effective to attain a desired purity of the silicone oil and conducting a low water vapor inert gas through said silicone oil during the reaction period; at the end of the reaction period, separating the drying agent and the adsorption agent from the silicone oil; said separation step comprising a sedimentation process and a filtering process.
Claim 2
Dependent Claim
130 words
Process for purifying silicone oil to remove impurities contained therein, comprising: adding a drying agent and an adsorption agent to the silicone oil, said adsorption agent selected from the group consisting of activated carbon and activated fuller's earth and said drying agent selected from the group consisting of molecular sieves, silica gel and activated aluminum oxide; causing the drying agent and the adsorption agent to act on the silicone oil during a reaction period effective to attain a desired purity of the silicone oil and conducting a low water vapor inert gas through said silicone oil during the reaction period; at the end of the reaction period, separating the drying agent and the adsorption agent from the silicone oil; said separation step comprising a sedimentation process and a filtering process.
Claim 3
Dependent Claim
32 words
Process for purifying silicone oil as defined in claim 1 wherein said step of causing comprises maintaining the silicone oil in movement for preventing sedimentation of at least one of the agents.
Claim 4
Dependent Claim
32 words
Process for purifying silicone oil as defined in claim 1 wherein said step of heating is carried out at a temperature which lies in a range from 50° C. to 110° C.
Claim 5
Dependent Claim
24 words
Process for purifying silicone oil as defined in claim 3 wherein said step of heating is carried out at a temperature of 95° C.
Claim 6
Dependent Claim
22 words
Process for purifying silicone oil as defined in claim 1 wherein the inert gas is gaseous nitrogen generated by heating liquid nitrogen.
Claim 7
Dependent Claim
42 words
Process for purifying silicone oil as defined in claim 1 wherein the inert gas is nitrogen and further comprising, before said step of conducting, heating the nitrogen to a temperature which lies in a temperature range from 20° C. to 80° C.
Claim 8
Dependent Claim
49 words
Process for purifying silicone oil as defined in claim 1 wherein the inert gas has a water content less than 0.1 ppm and said step of conducting is carried out until the water content of the silicone oil has been reduced to a value of less than 1 ppm.
Claim 9
Dependent Claim
34 words
Process for purifying silicone oil as defined in claim 1 wherein the inert gas is gaseous nitrogen, and said step of separating comprises conducting gaseous helium through the silicone oil to remove remaining nitrogen.
Claim 10
Dependent Claim
32 words
Process for purifying silicone oil as defined in claim 1 wherein the inert gas is gaseous nitrogen and said step of separating comprises ultrasonically exciting the silicone oil to remove remaining nitrogen.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-04-27 | 1990-10-27 | 1991-04-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-04-27 | 1994-10-27 | 1995-04-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-04-27 | 1998-10-27 | 1999-04-28 | $7700.00 | Window Closed / Lapsed |